Global Patent Index - EP 3586645 A1

EP 3586645 A1 20200101 - SYSTEM AND METHOD FOR PRODUCING AN EXTRUDED PROTEIN PRODUCT

Title (en)

SYSTEM AND METHOD FOR PRODUCING AN EXTRUDED PROTEIN PRODUCT

Title (de)

SYSTEM UND VERFAHREN ZUR HERSTELLUNG EINES EXTRUDIERTEN PROTEINPRODUKTS

Title (fr)

SYSTÈME ET PROCÉDÉ DE PRODUCTION D'UN PRODUIT DE PROTÉINE EXTRUDÉ

Publication

EP 3586645 A1 20200101 (EN)

Application

EP 19188029 A 20140731

Priority

  • US 201414308118 A 20140618
  • EP 14750946 A 20140731
  • US 2013054145 W 20130808
  • US 2014049137 W 20140731

Abstract (en)

The present invention relates to an elongated cooling die for an extruder, the die comprising the elongated die having an internal longitudinal channel configured to receive a stream from the extruder, the longitudinal channel having a transverse cross-section that is a continuous loop along at least a portion of the length of the die, the channel having a length and gap thickness configured to form oriented fibers from the protein component in a generally parallel orientation to produce the extruded protein product, wherein the ratio of the length of the channel to the gap thickness of the channel is between about 30:1 and about 1000:1, wherein the outer diameter of the channel is between about 200 and about 750 mm, and the gap thickness of the channel is between about 5 mm and about 30 mm, wherein the die includes one or more cooling apparatuses that cools the inner surface of the channel, and a support supporting the inner portion within the outer portion at one or more points along the length of the die.

IPC 8 full level

A23J 3/14 (2006.01); A23J 3/00 (2006.01); A23J 3/22 (2006.01); A23L 13/40 (2016.01); A23P 30/20 (2016.01)

CPC (source: EP KR US)

A23J 3/04 (2013.01 - EP KR US); A23J 3/14 (2013.01 - EP KR US); A23J 3/227 (2013.01 - EP KR US); A23J 3/26 (2013.01 - KR US); A23L 33/17 (2016.07 - EP KR US); A23P 30/20 (2016.07 - EP KR US); A47J 9/007 (2013.01 - KR US); B29C 48/022 (2019.01 - EP KR US); A23J 3/265 (2013.01 - US); A23V 2300/16 (2013.01 - KR); B29K 2089/00 (2013.01 - KR US); B29L 2031/748 (2013.01 - KR US)

Citation (applicant)

  • US 5922392 A 19990713 - KELLY LEO [GB], et al
  • US 2007269583 A1 20071122 - MCMINDES MATTHEW K [US], et al
  • US 2009291188 A1 20091126 - MILNE JEFFREY J [US], et al
  • US 2012093994 A1 20120419 - HSIEH FU-HUNG [US], et al
  • EP 1778030 A1 20070502 - SOLAE LLC [US]
  • EP 1059040 A1 20001213 - BONGRAIN SA [FR]
  • WO 03007729 A1 20030130 - CLEXTRAL [FR], et al
  • MEGARD ET AL.: "Continuous restructuring of mechanically deboned chicken meat by HTST extrusion cooking", JOURNAL OF FOOD SCIENCE, vol. 50, 1985, pages 1364 - 9, XP001349659
  • "High moisture extrusion with a twin-screw extruder: Fate of soy protein during the repetition of extrusion cooking", ISOBE AND NOGUCHI, NIPPON SHOKUHIN KOGOYO GAKKAISHI, vol. 34, 1987, pages 456 - 61
  • GWIAZDA ET AL.: "Microstructure studies of texturized vegetable protein products: Effects of oil addition and transformation of raw material in various sections of a twin screw extruder", FOOD MICROSTRUCTURE, vol. 6, 1987, pages 57 - 61
  • AOKI ET AL.: "Texturization of surimi using a twin-screw extruder", NIPPON SHOKUHIN KOGYO GAKKAISHI, vol. 36, no. 9, 1989, pages 748 - 53
  • "Noguchi, in Extrusion Cooking", 1989, AMERICAN ASSOCIATION OF CEREAL CHEMISTS, article "Extrusion cooking of high moisture protein foods"
  • CHEFTEL ET AL.: "New protein texturization process by extrusion cooking at high moisture levels", FOOD REVIEWS INTERNATIONAL, vol. 8, no. 2, 1992, pages 235 - 75, XP000372089
  • THIEBAUD ET AL.: "Influence of process variables on the characteristics of a high moisture fish soy protein mix texturized by extrusion cooking", LEBENSM.-WISS. U.-TECHNOL., vol. 29, 1996, pages 526 - 35

Citation (search report)

Designated contracting state (EPC)

AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

DOCDB simple family (publication)

US 2015044334 A1 20150212; US 9877498 B2 20180130; AU 2014304978 A1 20160303; AU 2014304978 B2 20171214; CA 2920387 A1 20150212; CA 2920387 C 20230124; CN 105530820 A 20160427; CN 105530820 B 20200331; CN 111264680 A 20200612; CN 111264680 B 20230505; DK 3030092 T3 20200518; DK 3586645 T3 20210712; EP 3030092 A1 20160615; EP 3030092 B1 20200226; EP 3586645 A1 20200101; EP 3586645 B1 20210421; ES 2788629 T3 20201022; ES 2880812 T3 20211125; JP 2016532447 A 20161020; JP 2020000235 A 20200109; JP 6560672 B2 20190814; JP 6781309 B2 20201104; KR 102321326 B1 20211103; KR 20160068733 A 20160615; MY 177094 A 20200905; PL 3030092 T3 20200824; PL 3586645 T3 20211206; US 10321702 B2 20190618; US 10798950 B2 20201013; US 2018098557 A1 20180412; US 2019289877 A1 20190926; WO 2015020873 A1 20150212

DOCDB simple family (application)

US 201414308118 A 20140618; AU 2014304978 A 20140731; CA 2920387 A 20140731; CN 201480050642 A 20140731; CN 202010171349 A 20140731; DK 14750946 T 20140731; DK 19188029 T 20140731; EP 14750946 A 20140731; EP 19188029 A 20140731; ES 14750946 T 20140731; ES 19188029 T 20140731; JP 2016533337 A 20140731; JP 2019132917 A 20190718; KR 20167005778 A 20140731; MY PI2016700457 A 20140731; PL 14750946 T 20140731; PL 19188029 T 20140731; US 2014049137 W 20140731; US 201715838562 A 20171212; US 201916438738 A 20190612